RU2506744C2 - Improvement of oxygen enrichment of fluid - Google Patents

Abstract

FIELD: agriculture.

SUBSTANCE: invention relates to a method and device for oxygen enrichment of a fluid. A method and unit (100, 206, 222) are proposed for obtaining the oxygen-enriched fluid. In accordance with various versions a flow of pressurised fluid (102, 124) is provided. In the flow of pressurised fluid a flow (114, 122) is introduced to obtain a mixture (126) of fluid/oxygen. The mixture is passed through the Venturi nozzle (134, 136) as an assembly in the presence of a magnetic field generated by the adjacent magnet unit (152, 154). Then the mixture is directed from the Venturi nozzle as an assembly into the container (164) for separating gas from fluid, in which the fluid component of the mixture passes down (170) with the specified content of dissolved oxygen, and the gas component is directed upwards (176) for injecting into the flow of the pressurised fluid.

EFFECT: use of the invention enables to obtain the fluid containing dissolved oxygen.

20 cl, 10 dwg

Description

Field of technology and prior art

This application is generally aimed at improving the enrichment of a fluid, such as, but not limited to, water, oxygen. There is still widespread interest in producing fluids containing dissolved oxygen. One effective method for producing oxygen-enriched fluid is discussed in US Pat. No. 6,821,438 to Hadley et al., Assigned to the applicant of this patent application and incorporated herein by reference.

In the Hadley patent, a fluid, such as water, is subjected to a series of process steps during which the fluid and oxygen introduced into it are passed through a high-speed venturi nozzle assembly and subjected to a strong magnetic field. It was shown that using this method, the rate of oxygen absorption and the durability of dissolved oxygen exceed these indicators for other methods of oxygen enrichment of the prior art.

Given the constant demand for fluids containing dissolved oxygen, including but not limited to drinks, such as water, there remains a continuing need to improve the method by which oxygen can be dissolved in and retained in the fluid. It is for such and other improvements that various embodiments of the present invention are generally directed.

SUMMARY OF THE INVENTION

Various embodiments of the present invention are mainly directed to a method and apparatus for enriching a fluid with oxygen.

In accordance with various embodiments of the present invention, a compressed fluid stream is obtained. An oxygen stream is introduced into the compressed fluid stream to form a fluid / oxygen mixture. This mixture is passed through a venturi nozzle assembly in the presence of a magnetic field that creates an adjacent magnetic block. The mixture then flows from the Venturi nozzle assembly into a container for separating gas from the liquid, in which the liquid component of the mixture goes down with a predetermined dissolved oxygen content, and the gas component is sent back to the introduction of compressed fluid into the stream.

These and other aspects of various embodiments of the present invention will become apparent upon consideration of the following detailed description and the accompanying drawings.

Brief Description of the Drawings

Figure 1 presents a functional block diagram of an oxygen enrichment system designed and operating in accordance with various embodiments of the present invention.

Figure 2 shows a table with an exemplary list of colloidal minerals suitable for use in the system of Figure 1.

Figure 3 shows the diffuser used in the system of Figure 1.

Figure 4 shows the mixer of the system of Figure 1.

FIGS. 5A-5B show, respectively, a side view and a vertical section of a venturi nozzle assembly of the system of FIG. 1.

Figure 6 shows two Venturi nozzle assembly, connected in series.

Figure 7 shows a vertical section of a gas-liquid separator of the system of Figure 1.

FIG. 8 is a functional block diagram of another embodiment of the present invention in which an oxygen enrichment system similar to that shown in FIG. 1 is used to provide oxygen-enriched water at the inlet of a fish tank in industrial fisheries.

Figure 9 shows a functional block diagram of another embodiment of the present invention, in which an oxygen enrichment system, similar to the system shown in Figure 1, is used to supply oxygen-enriched fuel at the inlet to the burner in industrial equipment.

10 is a graph depicting oxygen concentration levels in oxygen-enriched water obtained in accordance with various embodiments of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

Figure 1 shows a functional block diagram of an oxygen enrichment system 100 designed and operating in accordance with various embodiments of the present invention. The system of FIG. 1 is characterized as a relatively large-scale bottling system that releases significant quantities of bottled water. Water is dispensed into ordinary sealed plastic bottles or other suitable containers, and bottled water maintains the required concentration of dissolved oxygen.

While the currently preferred embodiments of the present invention are aimed at enriching water with oxygen, it should be understood that this case is not limiting; for example, the system 100 of FIG. 1 can be readily adapted to enrich other types of fluids with oxygen, such as, but not limited to, sports drinks, energy drinks, carbonated soft drinks, etc. Processed fluid may be prepared for human consumption or for other purposes.

A water source 102 is initially provided for supplying water to the system 100. In some embodiments, the water supplied from the source 102 is subjected to reverse osmosis treatment. The so-called "OO water" can have a total dissolved solids (ODS) of about 5-20 ppm (ppm, or milligrams per liter, mg / L). At this stage, other water treatment can also be carried out, including the use of ultraviolet (UV) light, filtration, etc., in order to reduce the level of microbes or otherwise prepare the water for processing.

Alternatively, the water from source 102 can be deionized to give the so-called “DI water”, which essentially lacks an RTOS. In other embodiments, water is supplied from a city water treatment system, from a natural source, from a river, or from some other source, during preliminary preparation, if necessary. In general, it is desirable to establish and control within reasonable limits the characteristics of the source water so that various parameters of the system 100 can be configured for a particular source water.

Water from source 102 can be pumped by pump 103, or otherwise dispensed at an appropriate pressure, for example, about 344.5 kPa (50 psi), and sent to refrigerator 104. The refrigerator reduces the water temperature to an appropriate level. Refrigerator 104 may use any compressed refrigerant or other water cooling mechanism.

In general, it has been found that colder water may be more susceptible to the reception and retention of dissolved oxygen. In some embodiments, the water is cooled to a well-controlled temperature level, for example, about 10-13 ° C (50-55 ° F). During the cooling process, the water temperature can be lowered by about 6-14 degrees Celsius (10-25 degrees Fahrenheit). Water can be passed through a series of coils to increase the residence time and the degree of heat removal from the water in the flow process, or water can be accumulated in the tank and taken from it downstream, if necessary.

Chilled water can be pumped by means of a liquid pump 105 constant pressure in the tank 106, where the reaction with ozone. Although it is shown in the case of system 100 that pumps 103, 105 are used, it is contemplated that it is also possible to supply liquid to system 100 from a pressure tank, from a domestic water supply system, etc., at an appropriate initial pressure so that no additional pressure is required to move system fluid.

In the reaction vessel 106, a certain amount of ozone (O ₃ ) is introduced into the water for disinfecting purposes. In some embodiments of the invention, a venturi nozzle 108 or other input means may be used to introduce ozone from the ozone generator 110. Excess oxygen and ozone from the reaction vessel 106 are discharged into the excess oxygen line to return the remaining oxygen to the oxygen vessel, at position 188.

Colloidal minerals from a source of 112 colloidal minerals are introduced into a mixture of water and ozone leaving tank 106. As discussed in more detail in the aforementioned Haclley patent, colloidal minerals provide electrostatic surface ion absorption characteristics, which can improve the ability of water to absorb and retain introduced oxygen. The amount and type of colloidal minerals added to water depends on the requirements of the particular application.

In some embodiments of the invention, colloidal minerals are obtained from TRC Nutritional Laboratories, Inc., Tulsa, Oklahoma, USA under the trademark TRC Minerals ®. The corresponding composition of 77LPPM TRC Minerals is shown in the table in figure 2. This composition can be delivered in 207.9 liter drums (55 gallons); it has a low content of microbiological constituents, the pH is from about 2.6 to 3.8, and it is colored pale yellow / tan.

Water and a mixture of minerals are supplied as a liquid stream under pressure to the oxygen introduction unit 114. Block 114 operates in such a way that it introduces a stream of gaseous oxygen (O ₂ ) into the water at a predetermined rate and concentration to form a fluid / oxygen mixture. As shown in FIG. 3, a diffuser unit 116 may be used by which the incoming oxygen (represented by the flow arrow 118) is injected at high pressure through the porous unit 120 to produce fine bubbles 122 in the surrounding water 124.

As shown in FIG. 4, the resulting water / gas mixture 126 is guided through a passive mixer 128. This mixer includes a central conduit 130 with circumferentially arranged vanes 132 that cause controlled mixing and reduction of bubble size. This helps to ensure the distribution of gaseous oxygen in the mixture.

Next, FIG. 1 shows two venturi nozzles assembly numbered 134, 136. In some embodiments, the venturi nozzles 134, 136 assembly are nominally identical and installed in parallel. In other embodiments, a venturi assembly may be used with various configurations, costs, etc. Separate valves and flow controls can be provided so that either one or both of the venturi nozzles are in operation at the moment, depending on the requirements for the overall system performance. In general, the venturi nozzles 134, 136 may be configured as described in the Haclley patent.

FIGS. 5A and 5B show a complete Venturi nozzle 134 in more detail so that a central channel 138 is visible, transitioning from a first zone 140 with a full cross section to a second zone 142 with a limited cross section. In some embodiments, the first zone 140 may be a circular pipe (e.g., a PVC or metal pipe), and the second zone 142 may be an elliptical pipe, as shown in Fig. 5B. “Elliptical” means a cross-sectional shape in which the width is greater than the length, and this does not necessarily require constant curved surfaces. In some embodiments, parallel plates of plexiglass or similar base material, such as the plates indicated by 144, 146 in FIG. 4B, may be separated by expanders 148, 150 to form an elliptical second zone 142.

The magnets 152, 154 in the ceramic block must be placed near the second zone 142, forming a directly adjacent magnetic block so that the fluid passes through a strong magnetic field as it flows through the venturi nozzle 134 assembly. If desired, other types of magnetic blocks can be used, for example, rare earth magnets, electromagnets. After the fluid has been exposed to a magnetic field, it exits the second zone 142 and enters the third zone 156. In some embodiments, the third zone 156 has the same diameter and cross-sectional shape as the first zone 140. As shown in FIG. 5A, flow control wedges 158, 160 can be inserted into the respective pipelines of the first 140 and second 156 zones to reduce turbulence. Downstream, it is possible to further provide a grating 162 for creating a laminar flow, so as to cause the formation of a laminar fluid flow downstream.

While each of the separate parallel paths in FIG. 1 shows one venturi assembly 134, 136, in further embodiments, several venturi assemblies may be installed in series, such as, for example, the venturi nozzles 134A and 134B in FIG. 6. The use of multiple venturi nozzles in assembly, as in FIG. 6, increases the residence time during which the fluid passes through magnetic fields. If desired, other designs can be used, including a Venturi nozzle assembly with different geometric configurations, a Venturi nozzle assembly with different intensities and / or magnetic field configurations, etc. While in some embodiments the fluid passing through the venturi assembly collides with a magnetic flux oriented perpendicular to the direction of its flow, another orientation can be used based on empirical analysis.

Venturi nozzles assembly act as a linear flow accelerator, accelerating the flow of the water / gas mixture to supersonic speeds. The speed of sound in a two-phase mixture of liquid and oxygen bubbles is approximately 15 meters per second (50 ft / s), although it can vary with the concentration of liquid and oxygen in the mixture. In comparison, the speed of sound in air is approximately 330 meters / s (1,100 ft / s), and the speed of sound in water is approximately 1,500 meters / s (5,000 feet / s).

The speed of the mixture decreases sharply at the outlet of each Venturi nozzle assembly, returning to speeds below the speed of sound. A supersonic flow reduces the velocity to values below the speed of sound throughout a thin region called a shock wave. The shock wave breaks the oxygen bubbles into microscopic bubbles, accelerating the mixing of liquid and gas. Thus, by forcing the flow to pass through two or more venturi nozzles assembled in series, as shown in FIG. 6, overlapping successive supersonic-subsonic pulses can be achieved on the flow, which further improves oxygen retention.

Continuing to examine FIG. 1, after passing through nozzles 134. 136 of the venturi assembly, the fluid enters the reservoir 164 for separating gas from the liquid. The container 164 may have the configuration shown in general terms in FIG. 7 and includes a main chamber 166 into which an incoming fluid mixture is introduced through an inlet 167 to the side of the middle partition wall 168. A partition, or screen, 168 divides the chamber into two halves , 166A and 166B. The incoming fluid fills the first half 166A of the chamber, after which the incoming fluid is poured through the baffle 168 into the second half of the chamber 166B and to the outlet 170.

This provides a controlled gas space 172 above the liquid, as well as aerating action through overflow through

a central dividing wall, depending on the relative levels of the fluid on each side of the central partition. The float valve device 174 moves vertically depending on the level of fluid / gas in the chamber 166. As the device 174 lowers, a fluid connection is established to the second outlet 176. Thus, the liquid portion of the inlet fluid (with substantially dissolved oxygen ) leaves the first opening 170, and excess, undissolved gas leaves through the second hole 176 for separation and reintroduction into the oxygen enrichment process downstream of the process stream.

Continuing to examine the flow in FIG. 1, the liquid exiting the first opening 170 is directed to a monitoring step 178, which may include a number of sensors and tracking devices, including a sensor for determining the amount of dissolved oxygen (PK) in the water. You can use a mass flow meter to control costs. In some embodiments, the control can be carried out optically, electrically, etc. Control modules must be designed to operate at pressures existing in a pressurized stream. At this stage, other monitoring data can be captured, as well as at other convenient locations along the process.

The fluid is sent to a bottling system 180, which places the appropriate amounts of oxygen-enriched water in the bottles, as shown at 182. Before being sent to end use, for example, to the bottling system 180, the fluid passes through an outlet control valve . Prior to the exhaust control valve, the approximate exhaust pressure may be approximately 206.7 kPa (30 psi). Bypass 184 allows you to return the excess of oxygen-enriched water to the corresponding previous position on the technological route.

The excess gas from the hole 176 (FIG. 7) flows in FIG. 1 to an ozone decomposition unit 186, which acts to decompose all the ozone contained in the gas and collect the remaining oxygen in an oxygen tank or in another tank in block 188 which supplies the incoming oxygen to the oxygen introduction unit 114. Block 188 can be used to produce oxygen from compressed air with a quality suitable for medical use, for example, with a purity level of about 90-93%. To supply the necessary oxygen from containers or other pressurized vessels, oxygen in cylinders 190 can be used.

It was found that the system 100 of FIG. 1 successfully provides dissolved oxygen levels of up to about 70 ppm (70 mg / L) or more. Dissolved oxygen exhibits substantially increased levels of stability; that is, water is capable of retaining significant levels of dissolved oxygen for extended periods of time, for example, over several months. As discussed above, a practical test showed dissolved (oxygen) levels of more than 40 ppm for bottled water with a shelf life of more than three months.

Fig. 8 depicts another embodiment of the apparatus of Figs. 1-7, and may include a number of components therein. 8, oxygen-enriched water is not intended for human consumption, like a drink, but for consumption by fish 202 (e.g., salmon, etc.) in fish tank equipment 200 in industrial fisheries.

As shown in FIG. 8, fresh water is supplied from a source 204, the same as the various sources listed above in FIG. 1. This fresh incoming water is sent to the oxygen enrichment unit 206, which may include the various steps shown in FIG. 1 (except for the bottling step and other appropriate steps) to produce an oxygen-enriched water stream. Such water may have an initial dissolved oxygen concentration of about 70 mg / L, or some other value. Depending on the application, this concentration can be considered too high for the health of the fish 202. Accordingly, oxygen-enriched water from block 206 can be diluted to a more suitable level, for example, about 5-14 mg / L, as shown by dilution line 208.

Since water in the tank can accumulate waste components, part of the water from the tank can be discharged and fed to the wastewater treatment unit 210, which can carry out the appropriate water treatment, including filtration, sedimentation (including the septic tank system (local wastewater treatment), etc. ), antibacterial treatment, elimination of nitrates, removal of CO ₂ , etc. The water treatment in block 210 may be a stream processing process, a local private processing system, etc. The treated water or any component thereof can then be introduced into the dilution line 208. Thus, the amount of fresh water necessary to maintain the fish population 202 in the tank 200 can be significantly reduced in comparison with systems of the prior art.

FIG. 9 shows another embodiment of an oxygen enrichment system 220 in which an oxygen enrichment method 222, somewhat similar to that of FIG. 1, is used to add a dissolved oxygen component to a combustible (eg, hydrocarbon) fuel from a source 224. The fuel can be heavy an oil product, such as diesel fuel, (or) a more volatile liquid fuel, such as gasoline. Some or many of the steps carried out in FIG. 1 can be used in processing step 222 to inject the desired amount of dissolved oxygen into the fuel, after which the mixture of fuel and oxygen is sent to burner 226 or some other process (for example, to an internal engine combustion, etc.).

Example

To enrich water with oxygen from the source, a full-scale (maximum 113.4 l / min (30 gallons per minute)) system was constructed corresponding to the system depicted in FIG. 1. The water from the source was subjected to the reverse osmosis process and filtered to 5 microns (5 × 10 ^-6 m) so that it had the following nominal characteristics (all values are approximate):

Total dissolved solids = 10-20 ppm;

pH = 6.1;

The initial level of dissolved oxygen = 7.2 mg / l, and

Temperature = 14 ° C (57 ° F).

Refrigerator 104 provided a reduction in temperature of the water from the source to 10 ° C (50 ° F). A constant pressure liquid pump 105 provided water from the source to the system at a pressure of 292 kPa (42.4 psi) at a rate of 30 l / min (7.9 gallons per minute).

The piping for the network between the pump 105 and the outlet to the bottling system 180 had a nominal diameter of 3.8 cm (1.5 inches). Ozone generator 110 supplied ozone through a Venturi nozzle 108 to an ozone reaction vessel 106 having a volume of 57 liters (15.1 gallons) and a maximum throughput of 150 l / min (39.6 gallons per minute). After the ozone reaction vessel 106, a fluid injection metering pump 112 provided colloidal minerals into the stream through a diffuser. The colloidal minerals used were those supplied by TRC Nutritional Laboratories, as discussed previously in connection with FIG. 2.

The flow rate of the introduced colloidal minerals was controlled in such a way as to create a total dissolved solids content of 20 to 50 ppm. Then the water and the mixture of minerals passed to oxygen supply unit 114, where oxygen from block 188 or oxygen from cylinders 190, or the combination was introduced through a diffuser block 116 at a pressure that was about 64 kPa (9.3 psi) higher than the water pressure.

Then, the resulting water / gas mixture flowed through the passive mixer 128 (FIG. 3) before entering the venturi nozzle assembly 134, in which the second zone 142 was formed by parallel Plexiglas plates 144, 146 spaced apart by approximately from 1 mm (0.04 inches) to 2 mm (0.08 inches) and having a length of about 150 mm and a width of about 80 mm (3.1 inches). When passing through the second zone 142, the flux was exposed to a strong magnetic field produced by two magnets 152, 154 in a ceramic block (100 mm (3.9 in.) × 50 mm (2.0 in.) × 25 mm (0.98 in.)) . Below the venturi nozzle 134, an upstream liquid / gas mixture passed through a laminar flow creating lattice 162 consisting of a bundle of tubes with a diameter of about 2 mm and typically 300 to 400 mm in length.

After passing through the laminar flow generating lattice 162, the liquid / gas mixture entered a 150 liter (39.6 gallon) gas and liquid separation vessel 164, from where excess, undissolved oxygen gas exited through a second outlet 176. Below the gas separation vessel 164 and The liquid flow passed through temperature, pressure and flow sensors before it was released through a flow control valve into a bottling device where 0.5 liter bottles (16.9 ounces) were filled at normal pressure.

An initial test was conducted to determine the “initial” oxygen concentration in water during bottling. These “source” samples showed dissolved oxygen levels in excess of 60 mg / L that are outside the measurement range of the dissolved oxygen hand-held instrument, which indicates a substantially 10-fold increase in the dissolved oxygen concentration for the starting samples compared to the concentration dissolved oxygen until oxygen enriches the water from the source.

Two crates, each with 24 bottles of bottled, oxygen-enriched water, were selected at Accurate Laboratories in Stillwater, Oklahoma, for long-term testing in an independent and certified laboratory. A representative selection of the results of these weekly tests is presented in FIG. 10. Half of the bottles were stored essentially at room temperature (for example, about 25 degrees Celsius), and the other half of the bottles were kept refrigerated (about 10 degrees Celsius). Two bottles stored at room temperature and two chilled bottles of water were opened every week for a 12-week period, and the contents were analyzed for dissolved oxygen.

All samples showed elevated levels of dissolved oxygen. Bottled, oxygen-enriched water that was stored at room temperature for 12 weeks showed a slight tendency to decrease dissolved oxygen concentration over time, although all dissolved oxygen concentrations at the end of the 12-week test period were 38 mg / L or higher. On the other hand, bottled, oxygen-enriched water, which was stored refrigerated, showed stable dissolved oxygen concentrations of about 50-60 mg / L, with a slight decrease in dissolved oxygen concentration or in the absence of a decrease, with continued testing.

Although it can be assumed that over time, when stored for longer than 12 weeks, there is a slight decrease in dissolved oxygen concentrations for chilled water, it follows from Figure 10 that the rate of this decrease may be relatively low. Thus, the results shown in FIG. 9 suggest that for water that has been subjected to an oxygen enrichment treatment in accordance with the discussion above, concentrations of dissolved oxygen in excess of 35 mg / L (and possibly significantly higher than 45 mg / l for chilled water). Despite the continuing need in industry for oxygen-enriched liquids with a long shelf life, the authors of this invention are not sure about the possibility of any other oxygen enrichment system giving a result that is at least somewhat close to this level of efficiency.

It should be understood that, in view of the discussion above, numerous other embodiments and applications of the present invention may exist for those skilled in the art, so that the preceding embodiments are merely illustrations of various possibilities, and are not limiting.

It should be understood that even if numerous features and advantages of various embodiments of the present invention were presented in the foregoing description, together with details of the structure and functions of various embodiments of the present invention, this detailed description is only illustrative, and changes in details can be made, especially with respect to the structure and organization of nodes, within the framework of the main ideas of the present invention, fully set forth in a broad general sense of the terms in which the attached form is expressed la inventions.

Claims (20)

1. A method of obtaining an oxygen-enriched fluid, comprising the following steps:
providing a compressed fluid flow;
introducing an oxygen stream into said fluid to form a fluid / oxygen mixture;
passing said fluid / oxygen mixture through a venturi nozzle assembly while exposing said mixture to a magnetic field from a magnetic block located in close proximity, and
passing said mixture from said Venturi nozzle assembly into a container for separating gas and liquid, in which the liquid component is passed further along the process stream with a predetermined dissolved oxygen content, and the gas component is sent back to introduce compressed fluid into said stream. 2. The method according to claim 1, wherein said introduction stage further comprises the step of passing said fluid / oxygen mixture through a passive mixer to provide controlled mixing and reduce the size of the bubbles of said fluid / oxygen mixture. 3. The method according to claim 1, further comprising the step of passing said fluid / oxygen mixture through two Venturi nozzles assembly used in parallel, such that a first portion of said fluid / oxygen mixture passes through the first of said Venturi nozzles assembly and the second a portion of said fluid / oxygen mixture passes through a second of said assembled venturi nozzles. 4. The method according to claim 1, further comprising the step of passing said fluid / oxygen mixture through multiple assembled Venturi nozzles arranged in series. 5. The method according to claim 1, further comprising the step of introducing colloidal minerals into said stream of said fluid before said stage of introducing said stream of oxygen into said liquid. 6. The method according to claim 1, wherein said step of providing a stream further comprises a step of cooling said stream of said fluid before the step of introducing it to a predetermined temperature of about 10 to 13 ° C. 7. The method according to claim 1, further comprising the step of extracting said gas component and supplying the gas component to an oxygen generator vessel, from which oxygen is supplied during said injection stage. 8. The method according to claim 1, wherein said fluid medium includes water. 9. The method according to claim 1, wherein said fluid with a specified predetermined dissolved oxygen content is bottled for human consumption. 10. The method according to claim 1, wherein said fluid with a specified predetermined dissolved oxygen content is fed into a container with a fish population. 11. The method according to claim 1, wherein said fluid with a specified predetermined dissolved oxygen content includes combustible fuel supplied to the burner. 12. The method according to claim 1, wherein said predetermined dissolved oxygen content is about 70 mg / L. 13. Installation for producing oxygen-enriched fluid, including:
a source supplying fluid to the system to form a compressed fluid stream;
a refrigerator in fluid communication with said fluid source, said cooler designed to reduce the temperature of said fluid stream to an appropriate temperature level;
the container in which the reaction occurs with ozone, which is in connection with the stream with the specified refrigerator; and in said container in which a reaction with ozone occurs, a certain amount of ozone is introduced into said fluid stream for disinfection purposes, which leads to the formation of a liquid / ozone mixture;
a source of colloidal minerals, which is connected downstream with the indicated container in which the reaction with ozone takes place, while this source provides the introduction of colloidal minerals into the specified liquid / ozone mixture;
an oxygen introduction unit, which is in a flow connection with a specified container in which a reaction with ozone takes place, and said oxygen introduction unit provides the introduction of gaseous oxygen into said liquid / ozone mixture, which leads to the formation of a liquid / gas mixture;
a complete venturi nozzle in fluid communication with said oxygen introduction unit and said liquid / gas mixture in said complete venturi nozzle is subjected to a magnetic field using a magnetic block, and
a container for separating gas and liquid, which is connected in a stream with the specified linear accelerator, in which the liquid component of the specified liquid / gas mixture is passed downstream of the process stream with a given dissolved oxygen content, and the gas component of the specified liquid / gas mixture is sent back for introduction into said compressed fluid stream. 14. The apparatus of claim 13, wherein said fluid is subjected to reverse osmosis treatment before being sent to a refrigerator. 15. The apparatus of claim 13, wherein said fluid includes water. 16. The apparatus of claim 13, wherein said fluid with said dissolved oxygen is bottled for human consumption. 17. The apparatus of claim 13, further comprising a passive mixer in fluid communication with said oxygen introduction unit and said passive mixer causes controlled mixing and bubble size reduction in said liquid / gas mixture. 18. The installation according to item 13, in which the specified Venturi nozzle Assembly includes:
a flat venturi nozzle having an internal cross-sectional area smaller than the corresponding cross-sectional area of the passage directly above and below said flat venturi nozzle along the process stream, and
a magnet adjacent to the said flat Venturi nozzle and passing along the main axis of the indicated cross-sectional area, which imposes a magnetic field of the required intensity on the specified stream in the specified flat Venturi nozzle, in which the specified flow is accelerated to high speed when passing through the specified Venturi nozzle, and then slow as this stream exits said venturi nozzle. 19. The apparatus of claim 18, wherein said magnet is a magnet in a ceramic block. 20. The installation according to item 13, in which the specified capacity for the separation of gas and liquid includes:
an inlet through which said liquid / gas mixture is introduced into the main chamber;
a partition that divides said main chamber into two halves, and said liquid / gas mixture fills the first half of said main chamber, after which said liquid / gas mixture is poured through said partition into the second half of said main chamber, and said liquid component of said liquid mixture / gas escapes through the outlet, and
assembly of the float valve, which is activated depending on the level of the liquid / gas mixture in the specified main chamber in such a way that as the specified float valve assembly is immersed, a flow connection is formed with the second outlet, and an excess of insoluble gas leaves from the specified second outlet for separation and re-introduction into the installation downstream of the process stream.

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